Abstract: A system for characterizing a slurry in a slurry process includes a flow tube, a camera, and a computer. The system is suitable for use with an oil sands extraction slurry processed or treated by an oil sands extraction slurry process. The slurry is diverted from the slurry process into the flow tube. The camera images the slurry as it flows through a transparent portion of the flow tube to produce a digital image of the slurry. The computer analyzes the digital image to determine a slurry characteristic. Based on the determined slurry characteristic, the computer may predict a performance metric of the slurry process and adjust an operating parameter of the slurry process to optimize the slurry process towards a target performance metric. Multiple systems may be used to continuously monitor slurry characteristics at upstream and downstream steps of the slurry process, and determine correlations between those characteristics.

Abstract: A system for characterizing a slurry in a slurry process includes a flow tube, a camera, and a computer. The system is suitable for use with an oil sands extraction slurry processed or treated by an oil sands extraction slurry process. The slurry is diverted from the slurry process into the flow tube. The camera images the slurry as it flows through a transparent portion of the flow tube to produce a digital image of the slurry. The computer analyzes the digital image to determine a slurry characteristic. Based on the determined slurry characteristic, the computer may predict a performance metric of the slurry process and adjust an operating parameter of the slurry process to optimize the slurry process towards a target performance metric. Multiple systems may be used to continuously monitor slurry characteristics at upstream and downstream steps of the slurry process, and determine correlations between those characteristics.

Abstract: Diluent-diluted bitumen froth containing bitumen and naphtha diluent, hydrocarbons, water, sand and fines (collectively “dilfroth”) is fed into a vapor-tight gravity settler (‘splitter’) and temporarily retained to produce a bottom layer of tails comprising sand and middlings, a rag layer of discrete three-dimensional structures, each comprising hydrocarbons contained in a skin of fines, and a top layer of hydrocarbons containing small droplets of water and fines (‘raw dilbit’). The flux in the splitter is less than 6 m3/h of dilfroth fed per m2 of horizontal cross-sectional rag area. The in-coming dilfroth is fed directly into the splitter middlings. Demulsifier is added to the overflow stream of raw dilbit and the mixture is subjected to prolonged settling in a vapor-tight polisher tank, to produce polished dilbit containing less than 1.0 wt. % water and 0.3 wt. % solids. The splitter underflow tails, containing less than 15 wt.

Abstract: Diluent-diluted bitumen froth containing bitumen and diluent hydrocarbons, water, sand and fines (collectively “dilfroth”) is fed into a gravity settler (‘splitter’) and temporarily retained to produce a bottom layer of tails comprising sand and middlings, a rag layer of discrete three-dimensional structures, each comprising hydrocarbons contained in a skin of fines, and a top layer of hydrocarbons containing small droplets of water and fines (‘raw dilbit’). The flux in the splitter is less than 6 m3/h of dilfroth fed per m2 of horizontal cross-sectional rag area. The in-coming dilfroth is fed directly into the splitter middlings. Demulsifier is added to the overflow stream of raw dilbit and the mixture is subjected to prolonged settling in a polisher tank, to produce polished dilbit containing less than 1.0% water and 0.3% solids.